analytical modeling of characteristic maps of the sr-30
TRANSCRIPT
Analytical Modeling of Characteristic Maps of the
SR-30 Turbojet Engine
Joaquín Valencia Bravo*, Frederick Just Agosto,
David Serrano Acevedo, Marco Menegozzo Department of Mechanical Engineering
University of Puerto Rico -Mayagüez
Mayagüez, Puerto Rico
Orlando Ruiz Quinones
Writing Systems Engineer, Hewlett Packard Inc.
Aguadilla, Puerto Rico
Abstract—A crucial step in the mathematical modeling of a
gas turbine engine is the characteristic map development of its
main components, the compressor and the turbine. Maps can
be obtained from manufacturers, although they are generally
not available to the user. Furthermore, the construction of
these maps through experiments is expensive. Analytical
models prove to be economically more advantageous.
Compared to other methods, they require little experimental
data to be validated. These models are based on physical
principles, so the results are more accurate compared to those
obtained through numerical simulations or the use of neural
networks. This approach allows more flexibility to make
changes to the performance characteristics of engine
components. These changes may be achieved by modifying
certain geometric measurements, this quality could be used in
diagnostic and/or engine control systems. In this work the
characteristic map of the SR-30 turbojet engine components is
analytically modeled. Geometric dimensions and properties of
the working fluid were taken as data. This is an one-
dimensional model in which it is analyzed the aerodynamics
and thermodynamics parameters in each station of the
centrifugal compressor and axial turbine. Design point
calculations are used to estimate the values of working fluid
parameters such as velocity, pressure, temperature, enthalpy,
and entropy function. Results of this work are compared with
those obtained by other authors. For greater reliability in
these results, an experimental validation is necessary.
Keywords — Turbojet engine; characteristic map; analytical
model; compressor; turbine
I. INTRODUCTION
Turbomachinery component performance maps constitute
an essential input to the development of engine
performance models. Maps may be obtained from
experimental procedures, but this can result in an expensive
endeavor. Furthermore, experiments might not completely
describe the full range of interest, and the use of
extrapolationis required. Manufacturers usually
developproduct component characteristic maps but this
information is rarely distributed to customers. In addition
to experimental methods, there are other alternatives in
obtaining performance maps. Kurzke [1] used data from
published maps to reproduce component maps through
commercial programs such as Smooth_C [2] and
Smooth_T [3]. Lazzaretto et al. [4] developed artificial
machine maps using generalized maps taken from literature
with appropriate scaling techniques. Results were
validated with test measurements from real plants. Many
authors have used neural networks approaches. Gustafson
el al. [5] obtained steady-state compressor performance
maps from correlations of transient compressor maps. The
learned correlations were expected to provide information
for predicting stall and surge inception. Yu et al. [6]
predicted an axial compressor's performance map based on
neural networks. Training was performed with
experimental results provided from manufacturers.
Ghorbanian et al. [7] used different types of neural
networks to simulate the performance maps of an axial
compressor; data was obtained from a compressor rig test.
Jiang et al. [8] developed an analytical model for the
centrifugal compressor based on first principles where
energy transfer is taken into consideration. The dynamic
performance including losses was determined from the
compressor geometry. In addition incident and friction
losses were modeled while the clearance, backward and
volute losses were considered constants for all off-design
conditions.Witkowski et al. [9] developed a one-
dimensional analysis for the SR-30 gas turbine components
used in education and research settings. Based on design
point performance, the flow through the radial compressor
and the one stage axial turbine was computed. The
corresponding initial conditions of the flow along with the
dimensions for each component were used. Losses were
estimated using Stodola's equation for slip factor
calculations. These calculations were only presented for a
design speed of 78000 rpm. Studies in developing the
component maps of a SR-30 turbine were performed by
various authors taking into consideration the design point
analysis developed by Witkowski et al. [9]. May et al. [11]
described a procedure to obtain the velocity triangles for
the characteristic maps of the SR-30 gas turbine. An
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iterative calculation in Excel was used, but the
mathematical analysis to achieve this goal was not
presented. Resulting maps were plotted using the Smooth-
C and Smooth-T commercial softwares. The model has
been used to monitor health operation of the engine. Based
on the mean-line analysis, Léonard et al. [10] developed
the compressor characteristic curves. The results were
stored in a line format to prevent numerical interpolation
problems. These authors did not use a map for the turbine,
instead, it was characterized using Stodola's ellipsis
equations. Compressor and turbine losses were considered
in the calculation of the velocity triangles. Oh et al. [11]
tested most of the loss models previously published in the
literature. They found an optimum set of empirical loss
models for a reliable performance prediction of centrifugal
compressors. May et al. [12] cites these loss correlations
for the calculation of the compressor map. In radial flow
machines, like centrifugal compressors, the angular
momentum imparted to the flow is reduced by a factor
known as the slip factor. von Backström [13] developed a
method that unifies the trusted centrifugal impeller slip
factor prediction methods of Busemann [14], Stodola [15],
Stanitz [16], Wiesner [20], Eck [17] and Csanady (reported
by Dixon [18]) in one equation. This equation, which is
used in the present work, may be adjusted for specifically
constructed families to improve the accuracy of the
prediction.There is no compressor map or turbine map
available for the SR-30 turbojet engine that has been
validated using experimental data.
The present work develops an analytical model of the SR-
30's component maps. A one-dimensional approach is
applied to perform the calculation at the design point
performance. The final goal is to produce tabulated
functions that may be introduced into an engine model. In
addition, interpolation will be applied to obtain values of
the dependent parameters such as the referred mass flow
rate m , the pressure ratio PR and the efficiency .
II. ANALYTICAL MODEL
In this section, the analytical model of the component maps
is described. The design point and off design performance
are conducted taking into account the limits of the engine
operation. Design point calculations are based on iterative
procedures. This consist on assuming a value of the axial
velocity component, then, performing the calculations
required to find the aero-thermodynamic properties of the
fluid and finally recalculating the assumed velocity.
Iteration is finished when the difference between the initial
guess and the calculated axial flow velocity is within the
imposed tolerance. As a result, the value obtained for the
remaining fluid parameters will be found. Compressor map
and turbine map models are described separately. The
properties of the working fluid in a gas turbine engine have
a powerful impact upon its performance. The working
fluid, which passes through the compressor, is assumed as
dry air and the working fluid that passes through the
turbine is assumed as the product of combustion; the
mixture of dry air and kerosene fuel. Water content due to
humidity is neglected. The correlations used for the fluid
properties were taken from Walsh et al. [19]. The equations
required to find the energy losses in the centrifugal
compressor was obtained from Oh et al. [11], and the loss
coefficients in the turbine, were taken from Dixon [18] and
Cohen et al. [20]. Moreover, the thermodynamic relations
used are derived from the Mollier diagram found in Dixon
[18].
A. Compressor Map
The SR-30 turbojet engine uses a centrifugal
compressor. The analysis for the flow through the
compressor is based in the one-dimensional steady flow
analysis, in which according to Dixon [18], the velocity
and density are regarded as uniform across each section of
a duct or passage. By continuity, the mass flow rate ( m )
through the compressor is given by
222222222111 ACACACACm aDDaDIIaIa ==== (1)
In equation (1), , Ca and A denote the air density, air
axial velocity and the cross-sectional area respectively. The
subscripts 1, 2I, 2D and 2 denote stations corresponding to
the entrance to impeller, exit from impeller, entrance to
vaned diffuser and the exit from vaned diffuser,
respectively. These stations can be visualized in Fig. 1.
Figure 1. Nomenclature of stations used in the compressor
Compressor maps will be developed from data points
obtained from calculations of the performance parameters
such as: mass flow rate m , rotational speed N, pressure
ratio PRc and isentropic efficiency c. For this purpose,
velocity triangles are calculated initially at the design point.
At this point, the mass flow rate and the rotational speed
are 297.0=m kg/s and N = 78000 rpm, respectively. In
addition, the geometric data and input conditions published
by Witkowski et al. [9] are used.
The first velocity triangle, depicted in Fig.2, is
calculated at the impeller inlet. According to this triangle,
the relation between the velocity vectors is given by
Figure 2. Velocity triangle at impeller inlet
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1 1 1= −V C U (2)
where V1 and C1 are the relative and absolute velocity
of the air, respectively. The term U1 denotes the impeller
eye velocity vector or tangential velocity vector. It is
assumed that the air enters the impeller eye in the axial
direction, i.e., 1 1a
C C= . The angle between the relative
velocity and the tangential velocity is 1=57. At the
impeller inlet (known also as eye or inducer), the effective
diameter is defined according to
( )2 2
1 0.5 t rD D D= + (3)
where Dt is the diameter at the impeller eye tip and Dr is
the diameter at the impeller eye root. The annulus area of
impeller eye is
( )2 2
14
t rA D D
= −
(4)
The mean tangential speed at the inducer may be
calculated by
1 1U D N= (5)
In addition, velocities at impeller eye tip (Ut=DtN) and
at impeller eye root (Ur=DrN) may be found. It is
important to check that the velocities at the impeller eye tip
should be less than the speed of sound (Mt< 1) to avoid
breakdown of flow and excessive pressure loss. To
calculate the axial component of the absolute velocity Ca1,
a trial and error process will be performed. Fig.3 shows the
iterative procedure followed to obtain the parameters at
compressor inlet or station 1, according to this flow
diagram, the density is calculated on the basis of the known
stagnation temperature and pressure. From the continuity
equation an initial estimate of the axial velocity Ca1 is
obtained. With this value and with the help of
thermodynamic relations from the Mollier diagram, the
density is recalculated, and the actual velocity is
determined from the continuity equation. If the assumed
and calculated velocities do not coincide, it is necessary to
iterate until convergence is reached.
Figure 3. Flow diagram of the iterative procedure at the impeller inlet
Equations required to calculate Ca1, are presented. The
static enthalpy h1 may be obtained by
1
2
01 1
1
2h h C= −
(6)
where 01
h is obtained from a polynomial function
dependent on the temperature T01, i.e. h01=fh(T01). The
static pressure p1 is given by
01 11
01
R
pp
e −
=
(7)
Here, p01 is the total pressure. The terms 01 and 1 are
functions dependent on the temperature T01 and T1, i.e. 01
=f (T01) and 1 =f (T1). The air density may be calculated
from the equation of state for a perfect gas, thus
1
1
1
p
RT =
(8)
where R is the gas constant for the air and T1 may be
found as a function of the enthalpy h1, i.e. T1 = fh (h1).
Finally, the axial velocity Ca1 is given by
1
1
1
a
mC
A=
(9)
Additional calculations are considered to obtain the
relative velocity V1, 2 2
1 1 1V C U= − and the absolute Mach
number, 1 1absM C RT= .
The velocity triangle at the impeller tip is shown in
Fig.4.
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Figure 4. Velocity triangle at impeller outlet
According to Fig. 4, the air leaves the impeller tip with
an absolute velocity C2I. This velocity has a tangential or
whirl component Cw2I and a small radial component Cr2I ,
they are related by
2
2 2
2 2I w I r IC C C+= (10)
Under ideal conditions the whirl component will be
equal to the impeller tip speed U2I . Due to the relative
eddies in the impeller blade passage the impeller exit flow
angle differs from the impeller exit blade angle; a measure
of deviation can be calculated using the concept of a slip
factor. There are many correlations predicitng the slip
factor. Von Backström [13] describes a method that unifies
the centrifugal impeller slip factor (). The prediction
method of Dixon [18]), that uses one equation, will be
used. This equation is given by
( )
1
1 0.5cos
1
1o Se
F
= −
+
(11)
where Fo is a correction constant corresponding to the
compressor. This value is adjusted to improve the
accuracy of the prediction. The blade angle at impeller exit
is denoted by . The ratio given l/Se is known as the blade
row solidity. The blade length l and blade spacing Se are
determined with ( )e i- / cosl = r r and /e e b= 2 r nS . The
terms ri and re are the radius of the blade leading edge and
blade trailing edge, respectively and the number of blades
is denoted by nb.The area at impeller exit, A2I, and the blade
speed U2I are calculated with 2 2 2I I I
A D b= and 2 2I I
U D N=
respectively. The terms D2I and b2I are the impeller tip
diameter and the axial width at impeller exit respectively.
In terms of the slip factor and the blade tangential speed,
the whirl component of the absolute velocity Cw2I are
determined with
2 2w I IC U= (12)
Some designers consider the value of the radial
component C2I the same as the inlet axial velocity Ca1
(Cohen et al.[20]), but, in the current model it is obtained
with an estimated value based on equation (10). The final
value of the radial component is determined following an
iteration procedure which is shown in Figure 5.
Figure 5. Flow diagram of the iterative procedure at the impeller outlet
According to the diagram shown in Fig. 5, static and
stagnation pressures and temperatures have to be
determined. Thus, the total pressure p02I is given by
02 01 2I Ip p PR= (13)
In equation (13), p01 is given as data and PR2I is the
pressure ratio. Initially PR2I is guessed and then calculated.
The stagnation temperature T02I may be obtained from a
correlation function of the stagnation enthalpy h02I, i.e.
( )0202 II ThT f= . The enthalpy h02I is given by
02
0201
01
2
IsI
I
h hh h
= +
− (14)
where h01 may be obtained from a correlation in
function of the stagnation temperature T01 which is given as
data. The term 2I denotes the efficiency that is initially
guessed and finally calculated after some iterations. The
stagnation enthalpy at an isentropic process h02Is is obtained
by the correlation function ( )0202 IsIs hTh f= . In the same
way, the temperature T02Is may be given by the correlation
function ( )0202 IsIs TT f = . The term 02Is is an entropy
function obtained by the following expression
02
02 01
01
ln IIs
pR
p = +
(15)
where the entropy function 01 is obtained using the
correlation function
( )01 01f T = . The static temperature
T2I is given in terms of the static enthalpy h2I with the
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correlation function ( )22 II ThT f= . The enthalpy h2I is
calculated with the expression
2
2
02 2
1
2I I Ih h C−=
(16)
The static pressure p2I is given by
02 2
202
I II
R
Ipp
e −
=
(17)
here the entropy functions 02I and 2I are given in term
of the temperatures T02I and T2I respectively, i.e.
( )0202 II Tf
= and ( )2 2I If T = .The density and the
radial component of absolute velocity are calculated using
( )22 2 II I RTp = and ( )2 22 I Ir I mC A= respectively. The Mach
numbers should be calculated to ensure that the flow does
not exceed the velocity of sound. The performance
parameters are also affected by losses that occur inside the
compressor. The correlations used for the compressor
losses were taken from Oh et al. [22] and Jiang et al. [8].
The pressure ratio and isentropic efficiency may be given
by
( )1
01
2 1
p
inteulerI
h hPR
c T
−
− = +
(18)
and
2
inteulerI
act
h h
h
− =
(19)
where, heuler is the ideal specific enthalpy change of the
working fluid which depends on the slip factor and the
tangential velocity of the blades at the impeller tip. Thus 2
2euler
Ih U = . The term
intΔh represents the summation
of all internal losses in the impeller such as incidence loss,
blade loading loss, skin friction loss and clearance loss,
thus int i bld f cl
Δh = Δh + Δh + Δh + Δhs
. The actual specific
enthalpy denoted by hact, is the sum of the ideal specific
enthalpy change and the parasitic loss correlations
(hact=heuler+hprs). The parasitic losses, hprs, are
assumed to be the sum of the disc friction loss,
recirculation loss and the leakage loss, i.e. hprs= hdf +
hrc +hlk.
The velocity triangle at the vaned diffuser inlet is
depicted in Fig. 6.
Figure 6. Velocity triangle at the vaned diffuser inlet
In Fig. 6, only the absolute velocity C2D and its
components are present. The relative velocity vanishes
because there is no moving element. To determine the
whirl component Cw2D of C2D, the conservation of the
angular momentum within the vaneless diffuser can be
assumed, i.e. Cw2D r2D = Cw2I r2I . Thus, the whirl
component of the velocity is given by
2 2
2
2
w I I
w D
D
C rC
r= (20)
The area and absolute velocity are obtained from A2D =
2r2D b2D and 2 2
2 22 r D w DDC C C= + respectively. The iterative
procedure performed here is similar to that followed at the
impeller exit. No further energy is supplied to the air after
it leaves the impeller, so that neglecting the
effect of friction, the angular momentum must be constant
(Cohen et al. [20]). The above implies that no work is done
in the vaneless diffuser and the process is adiabatic. Thus,
the following relation is obtained
02 02I D
h h= (21)
The pressure ratio and isentropic efficiency is calculated
in the same way as in the last stage. Although here, hintI is
substituted by hintVD which correspond to the losses in the
impeller and the vaneless diffuser, as follows: hintVD =
hintI +hvld.
Finally, calculations of the velocity triangle at the
diffuser output are performed. Here, the whirl component
of the velocity, is found using conservation of angular
momentum, which yields Cw2 = Cw2D r2D/ r2. The area and
the absolute velocity (magnitude) are A2 = 2 r2 b2 and 2 2
2 22 a wC C C= + respectively. The iterative procedure to
obtain the velocities and the thermodynamic states are
similar to the previous stations. Assumptions done for the
station of vaneless diffuser may be applied for the vaned
diffuser, thus h02D = h02. In the calculations of the pressure
ratio and the isentropic efficiency, the losses through the
entire compressor stage (i.e., impeller, vaneless diffuser
and vaned diffuser) have to be considered. These losses
denoted by hintT may be obtained by
hintT=hintVD+hiD+hsfD, where hintVD represents the
internal losses in the impeller and vaneless diffuser, hiD is
the incidence loss in the diffuser, and hsfD is the skin
friction loss in the diffuser.
The velocity triangles corresponding to the off-design
performance are constructed taking into account the mass
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flow rate and rotational speed in the range of
m = 0 - 0.5 kg/s and N =50000-90000rpm, respectively. In
the off-design calculations it is assumed that the absolute
inlet velocity remains axial and the design point value of
the slip factor was constant for all off-design conditions.
B. Turbine Map
The SR-30 is a single stage axial turbine composed of
one row of nozzles and one rotor. Figure 7 shows the
nomenclature of the stages employed in the calculations; N
refers to the nozzle and R the rotor.
Figure 7. Nomenclature of stations used for the turbine
Ainley and Mathieson correlations [18] were used to
calculate the energy losses. These estimated losses will be
useful in obtaining characteristic parameters such as the
mass flow rate m , the rotational speed N, the pressure ratio
PRt and the efficiency t. The operating conditions used in
establishing the design point velocity triangles were:
m = 0.3 kg/s and N=78000rpm. A mean annulus diameter
is assumed in the calculations. This approach is valid when
the ratio of the tip radius rt to the root radius rr is low (rt/rr
= 1:38). The turbine considered in this work meets this low
aspect ratio. Moreover, we can consider the mean diameter
equal in all stations because the difference between the
station mean diameters are negligible. Thus, the effective
mean diameter may be given by ( )2 2
m r tD = 0.5 D D+ . With the
effective diameter and the rotational speed, the mean blade
speed is U = DmN. The mean annulus area is calculated
by ( )2 2
r tmA = π D - D / 4 .
Geometric dimensions and inlet conditions were
extracted from Witkowski et al. [9]. By using the geometric
measurements of the turbine, a tip clearance of 0.54mm
was obtained. It is assumed that the stator blades have the
same shape as the rotor blades. The fluid through the
turbine is the air-fuel combustion products.
Fig. 8 depicts the velocity configurations at each station
in this turbine. In a single-stage turbine the velocity at
turbine inlet C3 will be axial (Cohen et al. [20]), thus, C3 =
Ca3 (Ca3 is the axial component of the velocity at turbine
inlet or station 3). The value of this velocity will be taken
as constant for all off-design conditions.
Figure 8. Velocity diagram of the axial turbine stage
Fig.9 shows the iterative procedure to calculate Ca3.
This procedure is similar to the calculations made at
compressor inlet.
Figure 9. Flow diagram of the iterative procedure at the nozzle inlet
Initially, the velocity Ca3 is guessed. Then, the static
temperature is found using a correlation in terms of the
static enthalpy h3, i.e. ( )3 T 3T = f h . The enthalpy h3 is
obtained by
3 03
2
3
1h = h - C
2 (22)
where: h03 = fh(T03, FAR) and FAR is the fuel-air ratio. The
static pressure is obtained using
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03 33
03
R
pp
e −
=
(23)
where 03=f(T03) and 3=f(T3). Similarly to previous
cases, the density is calculated with 3=p3/(RT3). From the
continuity equation, the axial velocity Ca3 is calculated by
a3 3 mC = m / (ρ A ) . Finally, the corresponding mach number
isdetermined using 3 33abs
C RTM = .
Fig. 8 shows the velocity triangle at the nozzle outlet or
station 4N. It is assumed that the nozzle angle (4N) and the
angular momentum at outlet remains constant. Therefore,
for all off-design conditions the deviation of flow across
the nozzle remains constant, thus 4N=constant. As a
result, the relationship between the whirl component Cw4N
and the axial component Ca4N (notation shown in Fig.8)
will be constant according to the relation.
4
4
4
1tan w N
N
a N
C
C
−=
(24)
Since no work is done (adiabatic process) by the gas in the
nozzle, the stagnation enthalpy must be constant over the
annulus at the outlet. Thus, h04N = h03. Fig.10 shows the
flow chart used for the iterative procedure to obtain the
axial component of the absolute velocity Ca4N.
Figure 10. Flow diagram of the iterative procedure at the nozzle outlet
According to this flowchart, the absolute velocity Ca4N
is guessed. Using this value and the angle 4N, the velocity
component Cw4N is obtained (Cw4N=Ca4Ntan4N). The
absolute velocity C4N is given by 2 2
4N a4N w4NC = C + C . The
static temperature T4N is found in term of the enthalpy, i.e.
( )44 NN ThT f= . The static enthalpy h4N is given by
4
2
04 4
1
2N N Nh h C−=
(25)
The static pressure may be calculated by
03 44
03
NsN
R
pp
e −
=
(26)
Where, ( )03 03,f T FAR = , ( )4 4 ,Ns Nsf T FAR = , and
( )4 4 ,Ns T NsT f h FAR= . The enthalpy under isentropic process
h4Ns is found using
4
2
44
2Ns
NN N
Ch h −=
(27)
where the total loss coefficient in the nozzle is denoted by
N. Neglecting the effect of friction, the critical pressure
ratio is
03
11
2c
p
p
− +=
(28)
If P03/P4N<P03/Pc, then the nozzle is not choked, otherwise,
it is chocked. The density 4N and the axial flow velocity
Ca4N are as follow 4N=p4N/(RT4N)
anda4N 4N mC = m / (ρ A )& . The absolute velocity and
relative flow angle are ( ) 2
44 4
2
4 a NN w NV C U C= − + and
4N=tan-1[(Cw4N-U4)/Ca4N].
The velocity triangle at rotor outlet or station 4 is depicted
in Fig. 8. The flow diagram of the iterative procedure at
this station is presented in Fig. 11.
Figure 11. Flow diagram of the iterative procedure at the rotor outlet
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According to this diagram, the exit angle 4 is constant
and it is calculated from the equations recommended by
Ainley and Mathieson (Dixon [18]), thus
441
11.5 1.154 coss
s e
− = − + +
(29)
In equation (29), is the throat width, s is the pitch and e is
the mean radius of curvature of the blade suction surface.
Equation (29) is for low outlet Mach numbers, i.e. 0 <
M4<0.5. If 4 1M the angle 4 is calculated using
( )41
cos s−
= . More details about this angle can be found
in Dixon [18]. Initially, the axial component of the absolute
velocity Ca4 is guessed using the equality Ca4=Ca4N. The
whirl component of the absolute velocity Cw4 may be
evaluated by
4 4 4 4tanw aC C U= − (30)
The absolute and relative velocity can be found similarly as
in the other stations. The static temperature is found by the
correlation ( )44 ,T
h FART f= . The static enthalpy h4 is given
by
4
2
404
2
Ch h −=
(31)
where h04 is calculated by
( )04 03 4 4 44
4 4
2tan tana N N
a
a N a N
U Ch h UC
C C+= − − (32)
In equation (32), the stagnation enthalpy h03 is obtained by
( )0303 ,h
T FARh f= .Using the stagnation enthalpy h04, the
stagnation temperature is computed with ( )0404 ,T
T FART f= .
The stagnation pressure is found from
0403
t
pp
PR=
(33)
where PRt is the total pressure ratio which is guessed
initially and then calculated by PRt=(03-04ss)/R . The
entropy function 03 is obtained using ( )0303 ,T FARf
= .
The stagnation entropy function 04ss is given by
( )0404 4 4ln
ss ssR p p+ = . The static entropy function 4ss
is obtained from the correlation ( )44 ,ssss T FARf
=
where the static temperature T4ss is calculated using the
correlation ( )44 ,ssss Th FART f= . The static enthalpy h4ss is
given by h4ss=h4s-(T4/T4N)(h4N-h4Ns). The static isentropic
enthalpy h4s is found using
4
2
44
2s R
Vh h −=
(34)
where R is the total loss coefficient in the turbine
rotor.The static pressure p4 was calculated with
04 44
04
R
pp
e −
=
(35)
here ( )0404 ,T FARf
= and ( )44 ,T FARf
= . The isentropic
efficiency is determined using
03 04
03 04
t
ss
h h
h h
−
−
=
(36)
The density and the axial velocity component are
calculated using equations similar to the previous cases. In
addition, the mach number M4 may be found by
4 44M = V RT . After doing the design point performance
analysis, the off-design performance is obtained varying
the speed and the mass flow rate. The speed was varied
from 50000rpm to 90000rpm and the mass flow rate was
varied until the design value was reached (0.3kg/s). The
deviation of flow across the nozzle is assumed as constant
at all off-design conditions. Because 4N is constant the
losses across the nozzle remain constant for all off-design
conditions.
III. RESULTS A. Compressor Map
Results of pressure, temperature, absolute velocity and Mach number in the behavior of the design point are shown in Table I. The values presented here correspond to each station in the compressor. The analysis was generated under the rotational speed of 78000rpm with a mass flow rate of 0.297kg/s. The abbreviation, PW, means present work. The table shows that the highest stagnation pressure is reached at the impeller outlet (P0 = 323kPa).Thepressure at the diffuser outlet is higher than the impeller inlet due to irreversibility. The compression work done by the impeller is accompanied by an increase in temperature, thus, the stagnation temperature at the impeller outlet is 446K. This temperature remains constant through the diffuser. Static pressure and static temperature gradually increase through the compressor. Thus, its maximum values are reached at the diffuser outlet, these are: 249kPa and 429K. The Mach number corresponding to the absolute velocity is maximum, and less than one, at the impeller outlet.
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Table I. Design pointperformance for the compressor
Parameter
Impeller inlet Impeller outlet
Diffuser inlet
Vaned
diffuser
outlet
1 2I 2D 2
Ref. [9]
PW Ref. [9]
PW Ref. [9]
PW Ref. [9]
PW
P0 (kPa) 100 100 323 323 319 307 269 287
T0 (K) 300 300 445 446 445 446 445 446
P (kPa) 93.6 93.6 167 183 200 191 269 249
T (K) 294 294.4 379 380 390 390 430 429
C (m/s) 106 106.3 366 366 335 337 176 188
Mabs 0.31 0.31 0.87 0.94 0.86 0.85 0.42 0.45
The results obtained correlate well with Witkowski et al.[9]. Calculations at impeller inlet, 1, are practically the same as those presented in [9]. Result differences in locations 2I, 2D, 2 are due to the correlations considered in the present work. The highest percent difference, corresponding to the static pressure at the impeller outlet, obtained when compared to [9] was 9.6%. This is most likely due to the difference in the energy loss and slip factor calculations. In the present work, correction factors were used in the energy loss calculations. The slip factor formula used in the present work was different from that used in Witkowskiet al. [9]. Furthermore, the coefficient F0 of the slip factor used was adjusted to obtain an appropriate value.
By varying the mass flow rate (0-0.55 kg/s) and the rotational speed (50,000 rpm - 90,000 rpm), the off-design performance was obtained. Fig. 12 shows the effect of variation of mass flow and rotational speed on the pressure ratio.
Figure 12. Compressor map: Pressure ratio vs mass flow rate
Solid curve lines shown in Fig. 12 are the rotational speed, these are indicated by dimensionless values that vary from 0.64 (50,0000 rpm) to 1.15 (90,000 rpm). These speed lines are obtained by joining pairs of points formed by the pressure ratio and the mass flow rate. The ends of each speed line coincide with the minimum and maximum mass flow rate. Joining imaginarily the minimum mass flow of each speed line it is obtained the surge line, this line is nearly at the left of the maximum efficiency line. Surging is associated with a sudden drop in delivery pressure, and with violent aerodynamic pulsation which is
transmitted throughout the whole machine. The line joining the maximum mass flow points for each rotational speed is called the choking line, that is, no further increase in mass flow is possible beyond this line.
Figure 13 shows the effect of variation of the rotational speed and the mass flow rate on the isentropic efficiency. Curved lines represent the rotational speed, indicated by dimensionless values. Speed lines values are the same as in Fig. 12. The operating point of maximum efficiency on each speed line is approximately the same. Ideally, the compressor should run on the curve connecting these points.
Figure 13. Compressor: Efficiency vs mass flow rate
In Fig. 12, eleven dashed lines intersect the speed lines
at a single point, these are called beta lines. Information on
mass flow, pressure ratio and efficiency is extracted from
each of these points. This information is taken in tabular
form, like Tables II, III and IV. These tables may be
introduced in a SR-30 turbojet engine model, this
procedure is presented in another work. Values of mass
flow rate, pressure ratio and isentropic efficiency of the
compressor are shown in tables II, III and IV, respectively.
The first column of these tables shows the enumeration of
beta lines. In the second row of each table, the percentage
values of the compressor rotational speeds are shown.
Table II. Tabulated values of the compressor mass flow rate.
β Rotational speed, N (%)
64 69 74 79 85 90 95 100 105 110 115
0 0.11 0.12 0.14 0.16 0.18 0.19 0.21 0.23 0.25 0.26 0.28
1 0.12 0.13 0.15 0.17 0.19 0.21 0.23 0.25 0.27 0.29 0.31
2 0.13 0.15 0.17 0.19 0.21 0.23 0.25 0.27 0.29 0.31 0.33
3 0.15 0.17 0.19 0.21 0.23 0.25 0.28 0.30 0.32 0.34 0.36
4 0.17 0.19 0.21 0.23 0.26 0.28 0.30 0.32 0.35 0.37 0.39
5 0.19 0.21 0.24 0.26 0.28 0.31 0.33 0.35 0.38 0.40 0.42
6 0.22 0.24 0.27 0.29 0.31 0.34 0.36 0.38 0.40 0.43 0.45
7 0.26 0.28 0.30 0.32 0.34 0.36 0.39 0.41 0.43 0.45 0.47
8 0.30 0.32 0.34 0.35 0.37 0.39 0.41 0.43 0.45 0.47 0.49
9 0.33 0.35 0.37 0.38 0.40 0.42 0.44 0.45 0.47 0.49 0.50
10 0.37 0.38 0.40 0.41 0.43 0.44 0.46 0.47 0.49 0.50 0.52
Table III. Tabulated values of the compressor pressure ratio
β Rotational speed, N (%)
64 69 74 79 85 90 95 100 105 110 115
0 1.68 1.68 1.68 1.67 1.66 1.63 1.60 1.56 1.50 1.44 1.37
1 1.81 1.82 1.82 1.81 1.80 1.77 1.73 1.68 1.62 1.55 1.46
2 1.98 1.99 1.99 1.97 1.95 1.92 1.88 1.82 1.74 1.65 1.55
3 2.16 2.17 2.17 2.16 2.14 2.10 2.05 1.98 1.90 1.79 1.66
4 2.37 2.38 2.38 2.37 2.34 2.30 2.24 2.16 2.06 1.93 1.78
5 2.62 2.63 2.62 2.60 2.57 2.52 2.45 2.37 2.25 2.11 1.93
6 2.90 2.90 2.89 2.87 2.83 2.77 2.70 2.60 2.46 2.30 2.09
7 3.21 3.21 3.19 3.17 3.12 3.06 2.98 2.88 2.75 2.57 2.27
8 3.56 3.55 3.53 3.50 3.45 3.39 3.30 3.20 3.07 2.86 2.40
9 3.95 3.94 3.91 3.88 3.83 3.77 3.69 3.59 3.42 3.05 2.51
10 4.38 4.37 4.34 4.30 4.26 4.19 4.11 3.96 3.67 3.19 2.65
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Table IV. Tabulated compressor efficiency values.
β Rotational speed, N (%)
64 69 74 79 85 90 95 100 105 110 115
0 75.5 77.7 78.5 78.2 76.9 74.6 71.3 67.0 61.5 54.7 0.46
1 75.4 77.7 78.7 78.6 77.5 75.5 72.5 68.5 63.3 56.7 0.49
2 76.2 78.1 79.0 78.8 77.7 75.7 72.8 68.9 63.8 57.3 0.49
3 76.4 78.3 79.1 79.0 78.1 76.2 73.5 69.8 64.9 58.6 0.51
4 77.9 79.6 79.3 79.2 78.3 76.5 74.0 70.3 65.6 59.4 0.53
5 77.6 79.0 79.5 79.3 78.3 76.7 74.2 70.8 66.3 60.4 0.53
6 78.3 79.3 79.6 79.3 78.3 76.7 74.4 71.2 66.8 61.1 0.53
7 79.0 79.5 79.6 79.2 78.3 76.8 74.8 72.1 68.5 63.5 0.54
8 79.4 79.6 79.5 79.0 78.1 76.9 75.1 72.9 70.0 64.9 0.53
9 79.5 79.5 79.3 79.0 78.2 77.2 75.9 74.0 70.7 63.2 0.51
10 79.3 79.3 79.1 78.8 78.2 77.3 76.1 73.8 70.0 60.2 0.49
Figure 14 compares the results obtained in the present work with those presented by May et al. [12]. The last one, indicated in the legend as paper. Three speed lines of the compression ratio versus mass flow rate graph were compared. The dimensionless values of these rotational speeds are 0.7 (54,000 rpm), 1 (78,000 rpm), and 1.1 (90,000 rpm). Results show a better match as speed increases. In the present work, when the compressor operates near the lowest rotational speed, the choking point is reached with a lower mass flow rate. As speed increases, results of speed lines between the two works match better.
Figure 14. Comparison of results for the compressor map.
B. Turbine Map
Table V shows comparative results between the present work, indicated by PW, and those presented by Witkowski et al. [9], indicated as Ref. [9]. Results are obtained in the design-point performance, that is, at a rotational speed of 78,000 rpm and a mass flow rate of 0.3 kg/s. As shown in the table, static and stagnation pressure decrease across each turbine location. The temperature is highest at the stator inlet. At this location, in the present work, the stagnation temperature is 973K while the static temperature is 967K. The Mach number reaches its maximum value at the stator output, this value is less than 1 (near the transonic region, M=1) in both results. If M=1,choking will occur. Both results match closely at locations 3 and 4N. It was evidenced that Witkowski et al. [9] has a mistake in the results of static pressure and static temperature, at location
3. A great difference between both results is observed in the absolute and relative velocities, at location 4. This may be due to the tip clearance value used to calculate the tip clearance loss. In the present work a value of 0.54 mm was used, this value was obtained by measurement carried out in the compressor of the experimental module. In Witkowski et al. [9] a value of 2.44 mm was used.
Table V. Design point performance for the turbine
Parameter
Stator inlet Stator outlet Rotor outlet
3 4N 4
Ref. [9]
PW Ref. [9]
PW Ref. [9]
PW
P0 (kPa) 250 250 234 229 120 120
T0 (K) 973 973 973 973 841 855
P (kPa) 94 244 128 128 115 106
T (K) 294 967 834 841 832 827
C (m/s) 114 114 557 550 141 250
Mabs 0.19 0.19 0.98 0.97 0.25 0.37
Off-design performance results are shown in Figures 15 and 16. Figure 15 shows the isentropic efficiency and mass flow rate against the work parameter, DH/T = (h4 - h3)/T3. In Fig. 15, each line represents the rotational speed. Colors identify the value of each of these speeds. As the speed increases, the maximum efficiency is reached at a higher value of the working parameter. For each speed, the efficiency remains approximately constant above a certain value of the working parameter. This behavior is due to the fact that the loss coefficients have a small variation in a wide range of incidence. Furthermore, this approximately constant efficiency is greater as the rotational speed increases.
Figure 155. Isentropic efficiency against work parameter.
In Fig. 16 it is observed that for each line of rotational speed, the maximum mass flow increases as the working parameter increases. An increase in mass flow occurs until choking conditions are reached. For all speed lines, choking occurs at the same mass flow rate and at a value of the working parameter greater than 100J-kg/K.
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Figure 166. Mass flow rate against workparameter.
In Fig. 17, results of the present work were compared
with those presented by May et al. [12], the latter named in the legend as paper.For this comparison, the relationship between mass flow rate and compression ratio was used. In this relationship, graphs of speed lines corresponding to 78,000 rpm are shown. The solid blue line is the one obtained in the present work while the red dashed line is the one obtained in May et al. Graphics are similar only in shape.The difference in the numerical values between both graphs is great. This is due to the fact that the maximum flow taken into account in May et al. [12] is close to 0.22 kg/s, while in this work 0.3 kg/s was considered. The value of 0.3 kg/s is more reasonable, since it represents the combustion mass flow that would be the sum of the air mass flow coming from the compressor plus the fuel mass flow entering the combustion chamber.
Figure 177. Comparison of results for the turbine map.
Tabulated values of mass flow rate and isentropic efficiency of the turbine are shown in tables VI and VII, respectively. The first column of these tables shows the values of the working parameter (DH/T or simply DHT). The second row of each table shows the percentage values of the rotational speeds of the turbine, these values are the same as for the compressor.
Table VI. Tabulated values of the turbine mass flow rate.
DHT Rotational speed, N (%)
64 69 74 79 85 90 95 100 105 110 115
10 0.17 0.18 0.19 0.19 0.20 0.21 0.22 0.22 0.23 0.24 0.24
25 0.21 0.22 0.22 0.22 0.23 0.23 0.24 0.24 0.25 0.25 0.26
40 0.24 0.25 0.25 0.25 0.25 0.25 0.26 0.26 0.27 0.27 0.27
55 0.27 0.27 0.27 0.27 0.27 0.27 0.27 0.28 0.28 0.28 0.28
70 0.29 0.29 0.29 0.28 0.28 0.28 0.29 0.29 0.29 0.29 0.29
85 0.30 0.30 0.30 0.29 0.29 0.29 0.29 0.29 0.29 0.30 0.30
100 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30
115 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30
130 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30
140 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30
150 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30 0.30
Table VII. Tabulated values of the turbine efficiency.
DHT Rotational speed, N (%)
64 69 74 79 85 90 95 100 105 110 115
10 74.4 72.8 71.1 69.2 67.3 65.4 63.4 61.4 59.5 57.5 0.56
25 78.3 78.4 78.2 77.8 77.2 75.8 75.7 74.8 73.9 72.8 0.72
40 76.5 77.4 78.0 78.3 78.4 78.2 78.2 78.0 77.5 77.0 0.76
55 73.6 75.2 76.3 77.2 77.8 78.4 78.4 78.5 78.5 78.4 0.78
70 70.6 72.6 74.2 75.4 76.4 77.7 77.7 78.1 78.4 78.6 0.79
85 67.5 69.9 71.9 73.5 74.8 76.7 76.7 77.3 77.8 78.2 0.78
100 64.4 67.2 69.4 71.4 73.0 75.4 75.3 76.2 76.9 77.5 0.78
115 62.3 64.4 67.0 69.2 71.1 74.0 74.0 75.0 75.8 76.6 0.77
130 62.3 64.3 66.1 67.7 69.2 72.4 72.4 73.7 74.7 75.6 0.76
140 62.3 64.3 66.1 67.7 69.2 71.7 71.7 72.8 74.0 75.0 0.76
150 62.3 64.3 66.1 67.7 69.2 71.7 71.7 72.8 73.8 74.7 0.75
IV. CONCLUSION
In this work, a one-dimensional analytical model of the compressor and turbine maps was made. The unified slip factor formula recommended by von Backström [13] was used. This formula was used in obtaining the whirl component of the absolute flow velocity at the outlet of the compressor impeller. In the compressor map calculations, the internal and parasitic loss correlations selected by Oh et al. [22] were used. In both maps calculations, iteration loops were used to find the axial component of the absolute flow velocity. Many equations were obtained from the Mollier diagram of the corresponding component. Finally, tabulated forms of the compressor and turbine maps were obtained. The results of the design point calculations for each component were compared with that presented by Witkowski et al. [9], a significant match was observed. Off-design performance results were compared with those obtained by May et al. [12]. These match well in the case of the compressor, turbine results showed similar behavior with a significant numerical values differing. This is most likely due to fact that May et al. [12] used a maximum flow rate of 0.22 kg/s while the calculation performed used a value of 0.3 kg/s. This value represents the combustion mass flow which would be the sum of both the air mass flow and the fuel mass flow entering the combustion chamber.
In order to further improve the modeling of the component maps, the validation should be developed by using experimental data or with maps obtained from manufacturers. In addition as built construction details should be used when ever available.
ACKNOWLEDGEMENTS:
The authors would like to acknowledge the interest and
encouragement of Dr. Allan Valponi. Views express in
this paper are those of the authors, and neither of persons
acknowledge herein nor of any funding source nor of their
institutions.
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